Methods of processing ß-lactoglobulin-containing compositions with thermolysin and transglutaminase

ABSTRACT

Methods of processing protein, methods of generating products with the processed protein, and products comprising and/or made with the processed protein. The methods of processing protein include hydrolyzing the protein with a proteolytic agent such as thermolysin to generate hydrolyzed peptides and, optionally, crosslinking the hydrolyzed peptides with a transglutaminase to generate crosslinked peptides. The methods reduce the allergenicity of allergenicity proteins such as β-lactoglobulin and casein. The methods of generating products with the processed protein include methods of making foams, emulsions, and/or food products with the processed protein. The products comprising and/or made with the processed protein accordingly include foams, emulsions, and food products. The foams, emulsions, and food products have decreased allergenicity compared to corresponding products made with non-processed proteins.

CROSS-REFERENCE TO RELATED APPLICATIONS

Priority is claimed to U.S. Application 62/674,186, filed May 21, 2018,which is incorporated herein by reference in its entirety.

FEDERAL FUNDING STATEMENT

This invention was made with government support under 2012-67017-30153and 14-CRHF-0-6055 awarded by the USDA/NIFA. The government has certainrights in the invention.

BACKGROUND

Food allergies continue to be a growing problem. Food allergies arehighly prevalent in children. Many children outgrow the allergies, butfor some, the milk allergies continue into adulthood.

Most people who suffer from food allergies have immune reactions tocertain proteins in the food. Strategies for reducing the allergenicityof such proteins include processing the protein with certain proteasesto destroy the allergenic epitopes on the proteins. In order to ensurethat these epitopes are disrupted enough to escape recognition from theimmune system, however, the proteins are very heavily processed, leavingsmall peptides that can only be incorporated in formulas and proteindrinks. These very small peptides also possess off flavors and smells.

Strategies for reducing the allergenicity of proteins that avoid theaforementioned problems are needed.

SUMMARY OF THE INVENTION

The invention is directed to methods of processing proteins. Theinvention comprises methods of hydrolyzing the protein with aproteolytic agent to generate hydrolyzed peptides and, optionally,crosslinking the hydrolyzed peptides with a transglutaminase to generatecrosslinked peptides. A preferred proteolytic agent is thermolysin,which is unexpectedly effective at reducing the allergenicity ofproteins, even with only partial hydrolysis of the protein. Crosslinkingthe hydrolyzed peptides further reduces allergenicity while generatingpolymerized structures suitable for incorporating into food products.The combination of hydrolyzing protein with thermolysin and crosslinkingwith transglutaminase can synergistically reduce allergenicity withrespect to the either step used alone. The thermolysin-hydrolyzed andcrosslinked peptides can be used to generate emulsions that are morestable than other protein- or peptide-based emulsions. Thethermolysin-hydrolyzed and crosslinked peptides can also be used togenerate foams. The resulting emulsions and foams are hypoallergenic. Itis predicted that the crosslinked peptides of the invention, and thefood products made therewith, have reduced off-flavors, smells, andallergenicity with respect to the non-crosslinked peptides.

The invention is also directed to products comprising the hydrolyzedpeptides and/or the crosslinked peptides made using the methodsdescribed herein. The products include food products that comprise thehydrolyzed peptides and/or the crosslinked peptides, emulsions thatcomprise the hydrolyzed peptides and/or the crosslinked peptides, foamsthat comprise the hydrolyzed peptides and/or the crosslinked peptides,and/or food products that comprise the emulsions and/or foams.

The objects and advantages of the invention will appear more fully fromthe following detailed description of the preferred embodiment of theinvention made in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A. Tricine-SDS-PAGE of WPI (whey protein isolate) and WPIhydrolysates produced under various substrate-to-enzyme ratios andhydrolysis times: Lane 1, WPI control; Lane 2, WPI+thermolysin, 2000:1,5 min; Lane 3, WPI+thermolysin, 1500:1, 5 min; Lane 4, WPI+thermolysin,400:1, 5 min; Lane 5, WPI+trypsin, 200:1, 30 min; Lane 6, WPI+trypsin,100:1, 30 min; Lane 7, WPI+trypsin, 100:1, 60 min; Lane 8,WPI+chymotrypsin, 200:1, 30 min; Lane 9, WPI+chymotrypsin, 100:1, 30min; Lane 10, WPI+chymotrypsin, 100:1, 60 min.

FIG. 1B. SDS-PAGE of WPI, WPI hydrolysates produced under specifiedoptimum substrate-to-enzyme ratios and hydrolysis times, and WPIhydrolysates repolymerized using transglutaminase (TGase). Lane 1, WPIcontrol; Lane 2, WPI+TGase; Lane 3, WPI+thermolysin, 1500:1, 5 min; Lane4, WPI+trypsin, 100:1, 30 min; Lane 5, WPI+chymotrypsin, 100:1, 30 min;Lane 6, WPI+thermolysin+TGase; Lane 7, WPI+trypsin+TGase; Lane 8WPI+chymotrypsin+TGase.

FIG. 1C. IgE reactivity of various enzyme-treated WPI products expressedon the basis of the immune-reactivity of WPI control. Statisticalanalysis was performed using Tukey HSD test. a-e: Mean values of columnswith different letters imply that they are significantly different(p>0.05).

FIG. 2A. SDS-PAGE profiles of peptides released from native WPI duringtime course of in vitro digestion under simulated gastric and duodenaldigestion conditions. The gastric digestion was performed for 60 min,followed by 180 min of duodenal phase digestion.

FIG. 2B. SDS-PAGE profiles of peptides released from thermolysin-WPIH-TGpolymers during time course of in vitro digestion under simulatedgastric and duodenal digestion conditions.

FIG. 2C. Immunoreactivity of peptides released during time course ofsimulated gastric and duodenal phase digestion of thermolysin-WPIH-TGpolymers.

FIG. 3A. SDS-PAGE of casein and casein hydrolysates produced undervarious substrate-to-enzyme ratios and hydrolysis times: Lane 1, Caseincontrol; Lane 2, casein+thermolysin, 2000:1, 5 min; Lane 3,casein+thermolysin, 1500:1, 5 min; Lane 4, casein+thermolysin, 800:1, 5min; Lane 5, casein+trypsin, 400:1, 10 min; Lane 6, casein+trypsin,200:1, 10 min; Lane 7, casein+chymotrypsin, 200:1, 10 min; Lane 8,casein+chymotrypsin, 100:1, 10 min.

FIG. 3B. SDS-PAGE of casein, casein hydrolysates produced underspecified optimum substrate-to-enzyme ratios and hydrolysis times, andcasein hydrolysates repolymerized using TGase. Lanes 1, casein control;Lane 2, casein+TGase; Lane 3, casein+thermolysin, 1500:1, 5 min; Lane 4,casein+trypsin, 400:1, 10 min; Lane 5, 5% casein+chyomotrypsin, 200:1,10 min; Lane 6, casein+thermolysin+TGase; Lane 7, casein+trypsin+TGase;Lane 8, casein+chyomotrypsin+TGase.

FIG. 3C. Immunoreactivity of enzyme-treated caseinate products.Statistical analysis was performed using Tukey HSD test. a-c: Meanvalues of columns with different letters imply that they arestatistically significantly different (p>0.05).

FIG. 4A. SDS-PAGE of peptides released from native casein during timecourse of in vitro digestion under simulated gastric and duodenaldigestion conditions. The gastric digestion was performed for 60 min,followed by 180 min of duodenal phase digestion.

FIG. 4B. SDS-PAGE of peptides released from thermolysin-CNH-TG polymersduring time course of in vitro digestion under simulated gastric andduodenal digestion conditions.

FIG. 4C. Immunoreactivity of peptides released during time course ofsimulated gastric and duodenal phase digestion of thermolysin-CNH-TGpolymers.

FIG. 5 . SDS-PAGE of enzyme-treated soy protein products: Lane 1, soyprotein isolate (SPI); Lane 2. SPI/TG; Lane 3, 10% SPI/thermolysin200:1, 30 min; Lane 4, 5% denatured SPI/trypsin, 100:1, 30 min; Lane 5,5% denatured SPI/chymotrypsin, 100:1, 30 min; Lane 6, 20% thermolysinhydrolysate/TG; Lane 7, 5% trypsin hydrolysate/TG; Lane 8, 5%chymotrypsin hydrolysate/TG.

FIG. 6 . Immunoreactivity of enzyme-treated soy protein products.Statistical analysis was performed using Tukey HSD. p<0.05 wasconsidered statistically significant. Different letters on top of thecolumns depict statistical difference.

FIG. 7 . SDS-PAGE of in vitro digested TG polymers of thermolysinhydrolysate of SPI.

FIG. 8 . IgE reactivity of in vitro digested TG polymers of thermolysinhydrolysate of SPI.

FIGS. 9A and 9B. SDS-PAGE of enzyme-modified WPI under reducing (FIG.9A) and non-reducing (FIG. 9B) conditions: FIG. 9A: Lane 1, MW standard;Lane 2, WPI; Lane 3, WPI-TG; Lane 4, WPIH; Lane 5, WPIH-TG. FIG. 9B:Lane 1, MW standard; Lane 2, WPI; Lane 3, WPI-TG; Lane 4, WPIH; Lane 5,WPIH-TG.

FIGS. 10A-10C2. Topographical AFM images of (FIG. 10A) native WPI,(FIGS. 10B1 and 10B2), WPI-TG, and (FIGS. 10C1 and 10C2) WPIH-TG at pH7. FIGS. 10B2 and 10C2 show expanded portions of FIGS. 10B1 and 10C1,respectively.

FIG. 11 . pH-turbidity profile of native WPI (square, ▪), WPI-TG(triangle, ▴), and WPIH-TG (diamond, ♦) samples in deionized water. Theprotein concentration was 0.1% (w/v).

FIG. 12 . Visual appearance of WPI-TG and WPIH-TG solutions (5% w/w) atpH 7.0 after centrifugation at 5000 g for 10 min.

FIG. 13A. Interfacial area decay of foams of native WPI (diamond, ♦),WPI-TG (circle, ▴), WPIH (triangle, ▴), and WPIH-TG (square, ▪) samples.The protein solutions (5% w/w) were made in 20 mM phosphate buffer, pH7.0. The error bars represent standard deviation of replicates.

FIG. 13B. Kinetics of adsorption of native WPI (diamond, ♦), WPI-TG(circle, ▴), WPIH (triangle, ▴), and WPIH-TG (square, ▪) at theair-water interface from a bulk phase (10 mM phosphate buffer, I=0.1M,pH 7.0) containing 10⁻⁴% (w/v) protein concentration.

FIG. 14 . Change in interfacial area of WPI (diamond, ♦), WPI-TG(circle, ●), WPIH (triangle, ▴), and WPIH-TG (square, ▪) emulsions overone-month storage at room temperature. The emulsions were prepared using1% (w/w) protein solution in 20 mM phosphate buffer, pH 7.0 and an oilvolume fraction of 20% (v/v).

FIGS. 15A-15H. Multimodal size distribution charts displaying change inparticle size distribution of emulsions of WPI (FIGS. 15A and 15B),WPI-TG (FIGS. 15C and 15D), WPIH (FIGS. 15E and 15F), and WPIH-TG (FIGS.15G and 15H) on day 1 (FIGS. 15A, 15C, 15E, and 15G) and on day 27(FIGS. 15B, 15D, 15F, and 15H).

DETAILED DESCRIPTION OF THE INVENTION

The invention, in part, is directed methods of processing proteins. Theproteins processed in the method can comprise any polypeptide, whetherpurified, semi-purified, or unpurified. The protein can comprise anywholly intact natural, recombinant, or synthetic polypeptide; anyprocessed forms thereof, including any denatured, cleaved, partiallydigested, or partially hydrolyzed forms; and/or any compositionscomprising same.

In some versions, the protein comprises an allergenic protein.“Allergenic protein” refers to any polypeptide capable of eliciting animmune response, such as an IgE response, in an animal. Allergenicproteins include any protein approved and officially recognized as anallergen by the Allergen Nomenclature Sub-Committee of the World HealthOrganization and International Union of Immunological Societies(WHO/IUIS), or any processed form thereof. See, e.g., Marsh et al.(Marsh D G, Goodfriend L, King T P, Lowenstein H, Platts-Mills T A.Allergen nomenclature. Bull World Health Organ 1986; 64:767-74), King etal. (King T P, Hoffman D, Lowenstein H, Marsh D G, Platt-Mills T A,Thomas W R. Allergen Nomenclature. 1994; 72:797-800. Bulletin WorldHealth Organization), King et al. (King T P, Hoffman D, Lowenstein H,Marsh D G, Platts-Mills T A, Thomas W. Allergen nomenclature. WHO/IUISAllergen Nomenclature Subcommittee. Int Arch Allergy Immunol 1994;105:224-33), King et al. (King T P, Hoffman D, Lowenstein H, Marsh D G,Platts-Mills T A, Thomas W. Allergen nomenclature. Allergy 1995;50:765-74), Larsen et al. (Larsen J N, Lowenstein H. Allergennomenclature. J Allergy Clin Immunol 1996; 97:577-8), Chapman et al.(Chapman M D. Allergen Nomenclature. In “Allergens and AllergenImmunotherapy” 3rd Edition. Editors, R F Lockey, S C Bukantz & JBousquet, pp 51-64, 2004. Marcel Decker), Chapman (Chapman M D. AllergenNomenclature. In “Allergens and Allergen Immunotherapy” 4th Edition.Editors, Richard F. Lockey, Dennis K. Ledford, pp 47-58. 2008. InformaHealthcare, New York), Larsen (Larsen J N. Allergen nomenclature: a needfor the scientific community. Arb Paul Ehrlich Inst Bundesamt SeraImpfstoffe Frankf A M 2006; 95:5-9), Chapman et al. (Chapman M D, PomésA, Breiteneder H, Ferreira F. Nomenclature and structural biology ofallergens. J Allergy Clin Immunol 2007; 119:414-20), Breiteneder H,Chapman M D. Allergen Nomenclature. In Allergens and AllergenImmunotherapy: Subcutaneous, sublingual and oral. 5th Edition. Edited byRichard F. Lockey and Dennis K. Ledford. CRC Press, Taylor and FrancisGroup, Boca Raton, Fla., USA, 2014, pp 37-49), Radauer et al. (RadauerC, Nandy A, Ferreira F, Goodman R E, Larsen J N, Lidholm J, Pomés A,Raulf-Heimsoth M, Rozynek P, Thomas W R, Breiteneder H. Update of theWHO/IUIS Allergen Nomenclature Database based on analysis of allergensequences. Allergy, 2014, 69(4):413-419). Such allergenic proteins canbe found in the WHO/IUIS database, accessible via www.allergen.org.

Examples of allergenic protein include milk protein, legume protein,tree nut protein, and grain protein. “Milk protein,” “legume protein,”“tree nut protein,” and “grain protein” refer to protein purified from,extracted from, obtained from, or contained in milk, legume, and grain,respectively. Examples of milk protein include whey protein isolate,which includes β-lactoglobulin, and casein, which includes β-casein.Examples of legume protein include soy protein and peanut protein, whichinclude allergenic cupins (Ara h 1), prolamins (Ara h 2, 6, 7, 9),profilins (Ara h 5), and Bet v-1-related proteins (Ara h 8).Commercially relevant forms of soy protein include soy protein isolateand soy protein concentrate. Examples of tree nut protein include Brazilnut protein, almond protein, chestnut protein, hazelnut protein, pinenut protein, and walnut protein, which comprise allergenic seed storageproteins (vicilins, legumins, albumins), plant defense-related proteins,and profilins. Examples of grain protein include wheat protein, barleyprotein, rye protein, triticale protein, and oat protein, which comprisegluten (variously also referred to as gliadin in wheat, hordein inbarley, secalin in rye, and avenin in oats).

The methods of processing proteins comprise a step of hydrolyzing theprotein with a proteolytic agent to generate hydrolyzed peptides. Asused herein, “hydrolyzing” broadly refers to any mechanism of cleaving agiven protein (polypeptide) into smaller polypeptides, regardless ofwhether or not water is consumed in the reaction. “Polypeptide” and“peptide” are used interchangeably herein.

In some versions, the protein comprises an allergenic protein, and thehydrolyzing is performed under conditions effective for the hydrolyzedpeptides to have reduced allergenicity with respect to the protein. Suchconditions include suitable enzyme concentrations, reaction time,reaction temperature, and solvent conditions (pH, salt concentration,etc.) all of which are ascertainable from a practitioner in the art inview of the following examples. “Reduced allergenicity” as used hereinrefers to a reduction in the ability to induce an immune response andcan occur through a reduction in IgE reactivity among other mechanisms.

The proteolytic agent may comprise any agent capable of cleaving a givenprotein into smaller polypeptides. Suitable proteolytic agents includenon-enzymatic proteolytic agents and enzymatic proteolytic agents.Non-enzymatic proteolytic agents include mineral acids such ashydrochloric acid, cyanogen bromide, BNPS-skatole, formic acid,hydroxylamine (NH₂OH), iodosobenzoic acid, trifluoroacetic acid, NTCB(2-nitro-5-thiocyanobenzoic acid), and others. Enzymatic proteolyticagents include proteases. Suitable proteases include any serineproteases, cysteine proteases, threonine proteases, aspartic proteases,glutamic proteases, metalloproteases, and asparagine peptide lyases.Exemplary suitable proteases include aeromonolysin, arg-C proteinase,asp-N endopeptidase, aureolysin, caspases (e.g., caspase 1, caspase 2,caspase 3, caspase 4, caspase 5, caspase 6, caspase 7, caspase 8,caspase 9, caspase 10), chymotrypsin, clostripain (clostridiopeptidaseB), enterokinase, factor Xa, glutamyl endopeptidase, granzyme B, lysClysyl endopeptidase (Achromobacter proteinase I), lysN peptidyl-lysmetalloendopeptidase, mycolysin, neutrophil elastase, pepsin,proline-endopeptidase, proteinase K, pseudolysin, Staphylococcalpeptidase I, tobacco etch virus protease, thrombin, and trypsin.

Particularly preferred proteases include thermolysins. “Thermolysin”refers to enzymes falling under Enzyme Commission (EC) number 3.4.24.27.Various thermolysins include the neutral proteinases from Bacillusthermoproteolyticus and Geobacillus stearothermophilus, and recombinantversions thereof. The terms “thermoase,” “thermoase Y10,” and “TLN” arealso used to refer to thermolysins. Thermolysins specifically catalyzethe hydrolysis of peptide bonds containing hydrophobic amino acids. Anexemplary thermolysin is commercially available from Sigma-Adrich (St.Louis, Mo.) under catalog number P1512.

Thermolysins are particularly effective in reducing the allergenicity ofprotein such as whey protein and other types of protein, both when usedalone and when used in combination with a translglutaminase. In certainversions of the invention, for example, thermolysins are capable ofhydrolyzing the protein into hydrolyzed peptides having an IgEimmunoreactivity less than 29% of the IgE immunoreactivity of theprotein, such as less than 28% of the IgE immunoreactivity of theprotein, less than 27% of the IgE immunoreactivity of the protein, lessthan 26% of the IgE immunoreactivity of the protein, less than 25% ofthe IgE immunoreactivity of the protein, less than 24% of the IgEimmunoreactivity of the protein, less than 23% of the IgEimmunoreactivity of the protein, less than 22% of the IgEimmunoreactivity of the protein, less than 21% of the IgEimmunoreactivity of the protein, less than 20% of the IgEimmunoreactivity of the protein, or less than 19% of the IgEimmunoreactivity of the protein.

In some versions of the invention, the hydrolyzing comprises onlypartially hydrolyzing the protein such that the resulting hydrolyzedpeptides are partially hydrolyzed peptides. “Partially hydrolyzing”refers to hydrolysis of protein with a given proteolytic agent to adegree of hydrolysis (DH) of less than 95% of the maximal degree ofhydrolysis obtainable with the given proteolytic agent. In variousversions of the invention, the protein is hydrolyzed to a degree ofhydrolysis of less than 90%, less than 80%, less than 70%, less than 60%less than 50%, less than 40%, less than 30%, less than 20%, less than10%, less than 1% of the maximal degree of hydrolysis obtainable withthe proteolytic agent used in the hydrolysis step. “Degree ofhydrolysis” as used herein refers to the proportion of cleaved peptidebonds in a protein hydrolysate and is determined according to thepH-Stat method (Adler-Nissen, J. (1986). Enzymatic hydrolysis of foodproteins. New York; Elsevier Applied Science Publishers).

In various versions of the invention, the hydrolyzing comprisespartially hydrolyzing the protein to a degree of hydrolysis of fromabout 0.001%, 0.01%, 0.1%, 1%, 2%, 5%, 10%, 20%, 30%, 40%, 50%, 60%,70%, 80%, 90%, 95% or more to less than about 1%, 2%, 5%, 10%, 20%, 30%,40%, 50%, 60%, 70%, 80%, 90%, 95% or more. Exemplary ranges include adegree of hydrolysis of from about 0.1% to about 10%, such as from about0.5% to about 5%, or from about 1% to about 3%.

In various versions of the invention, the hydrolyzing comprisespartially hydrolyzing the protein to generate partially hydrolyzedpeptides wherein a proportion of the total mass of the hydrolyzedpeptides comprise peptides having a particular size. For example, atleast about 5%, 10%, 15%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%,70%, 75%, 80%, 90%, 95%, or more of the total mass of the partiallyhydrolyzed peptides may comprises peptides having a size of from about0.5 kDa, 1 kDa, 2 kDa, 3 kDa, 4 kDa, 5 kDa, 10 kDa, 15 kDa, or 20 kDa toabout 5 kDa, 10 kDa, 25 kDa, 50 kDa, 75 kDa, or 100 kDa. In someversions, about 5%, 10%, 15%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%,65%, 70%, 75%, 80%, 90%, 95%, or more of the total mass of the partiallyhydrolyzed peptides comprises of from about 3 kDa to about 10 kDa. Theproportion of the total mass of the hydrolyzed peptides comprisingpeptides having a particular size is determined for the purposes hereinaccording to the size exclusion chromatography method of Adjonu et al.(Adjonu R, Doran G, Torley P, Agboola S. Screening of whey proteinisolate hydrolysates for their dual functionality: influence of heatpre-treatment and enzyme specificity. Food Chem. 2013 Feb. 15;136(3-4):1435-43).

An optional but preferred step in the methods described herein includecrosslinking the hydrolyzed peptides with a transglutaminase to generatecrosslinked peptides. A transglutaminase is an enzyme that catalyzes theformation of an isopeptide bond between a free amine group (e.g.,protein- or peptide-bound lysine) and the acyl group at the end of theside chain of protein- or peptide-bound glutamine. Such enzymes areclassified as EC 2.3.2.13. Transglutaminases are commercially availablefrom Sigma-Aldrich (St. Louis, Mo.) under catalog number T5398 andAjinomoto Food Ingredients (Eddyville, Iowa, USA).

In some versions, the protein originally hydrolyzed comprises anallergenic protein, the hydrolyzed peptides retain at least someallergenicity, and the crosslinking of the hydrolyzed peptides isperformed under conditions effective for the crosslinked peptides tohave reduced allergenicity with respect to the hydrolyzed peptides. Suchconditions include suitable enzyme concentrations, substrates, reactiontime, reaction temperature, and solvent conditions (pH, saltconcentration, etc.) all of which are ascertainable from a practitionerin the art in view of the following examples.

Crosslinking with a transglutaminase is particularly effective inreducing the allergenicity of hydrolyzed peptides generated fromhydrolyzing whey protein and other types of protein with a thermolysin.In certain versions of the invention, for example, transglutaminases arecapable of crosslinking hydrolyzed peptides to generate crosslinkedpeptides having an IgE immunoreactivity less than 53% of the IgEimmunoreactivity of the hydrolyzed peptides, such as less than 50% ofthe IgE immunoreactivity of the hydrolyzed peptides, less than 45% ofthe IgE immunoreactivity of the hydrolyzed peptides, less than 45% ofthe IgE immunoreactivity of the hydrolyzed peptides, less than 40% ofthe IgE immunoreactivity of the hydrolyzed peptides, less than 35% ofthe IgE immunoreactivity of the hydrolyzed peptides, or less than 30% ofthe IgE immunoreactivity of the hydrolyzed peptides.

In some versions of the invention, the protein comprises an allergenicprotein, and the hydrolyzing and the crosslinking are performed underconditions effective for the crosslinked peptides to have reducedallergenicity with respect to the protein. Such conditions includesuitable enzyme concentrations, substrates, reaction time, reactiontemperature, and solvent conditions (pH, salt concentration, etc.) allof which are ascertainable from a practitioner in the art in view of thefollowing examples.

The combination of hydrolyzing with a thermolysin and crosslinking witha transglutaminase is particularly effective in reducing theallergenicity of whey protein and other types of protein. In variousversions of the invention, for example, the combination of hydrolyzingwith a thermolysin and crosslinking with a transglutaminase, is capableof generating crosslinked peptides having an IgE immunoreactivity lessthan 31% of the IgE immunoreactivity of the protein, such as less than30% of the IgE immunoreactivity of the protein, less than 25% of the IgEimmunoreactivity of the protein, less than 20% of the IgEimmunoreactivity of the protein, less than 15% of the IgEimmunoreactivity of the protein, less than 10% of the IgEimmunoreactivity of the protein, or less than 7% of the IgEimmunoreactivity of the protein.

Hydrolyzing with a thermolysin and crosslinking with a transglutaminasein some versions is synergistically effective in reducing allergenicitycompared to the additive effects of each step taken individually.

The hydrolyzed and crosslinked peptides can be used in further steps togenerate certain products, such as food products, emulsions, and/oremulsions included in food products. The hydrolyzed and/or crosslinkedpeptides, for example, can be used to make emulsions by mixing thehydrolyzed peptides and/or the crosslinked peptides in an aqueous phasewith an oil phase to generate the emulsion. The emulsion can be anoil-in-water emulsion or a water-in-oil emulsion. As shown in theexamples, emulsions made with the hydrolyzed and/or crosslinked peptidesof the present invention have better storage stability then emulsionsmade with other types of polypeptides.

Various examples of food products that can include the hydrolyzed and/orcrosslinked peptides of the invention (either directly or in the form ofan emulsion) comprise protein shakes, infant formulas, soymilk, bread,and solid meat substitutes, such as tofu, tempeh, seitan, texturedvegetable protein, etc. It is predicted that the food products of theinvention will be less allergenic than corresponding food products madewith other protein sources. It is predicted that the food products ofthe invention will possess less potent or off flavors and smells thancorresponding food products made with other protein sources or willavoid them altogether. It is predicted that the structure of thecrosslinked peptides of the invention will permit the generation of morehighly structured food products (such as solid food products) thanhydrolyzed peptides.

The elements and method steps described herein can be used in anycombination whether explicitly described or not.

All combinations of method steps as used herein can be performed in anyorder, unless otherwise specified or clearly implied to the contrary bythe context in which the referenced combination is made.

As used herein, the singular forms “a,” “an,” and “the” include pluralreferents unless the content clearly dictates otherwise.

Numerical ranges as used herein are intended to include every number andsubset of numbers contained within that range, whether specificallydisclosed or not. Further, these numerical ranges should be construed asproviding support for a claim directed to any number or subset ofnumbers in that range. For example, a disclosure of from 1 to 10 shouldbe construed as supporting a range of from 2 to 8, from 3 to 7, from 5to 6, from 1 to 9, from 3.6 to 4.6, from 3.5 to 9.9, and so forth.

All patents, patent publications, and peer-reviewed publications (i.e.,“references”) cited herein are expressly incorporated by reference tothe same extent as if each individual reference were specifically andindividually indicated as being incorporated by reference. In case ofconflict between the present disclosure and the incorporated references,the present disclosure controls. The incorporation by referencespecifically includes but is not limited to U.S. Application 62/674,186,filed May 21, 2018; Damodaran et al. 2017 (Damodaran S, Li Y. A two-stepenzymatic modification method to reduce immuno-reactivity of milkproteins. Food Chem. 2017 Dec. 15; 237:724-732); and Chen et al. 2018(Chen A, Tanidjaja I, Damodaran S. Nanostructure and functionality ofenzymatically repolymerized whey protein hydrolysate. Food Chem. 2018Aug. 1; 256:405-412).

It is understood that the invention is not confined to the particularconstruction and arrangement of parts herein illustrated and described,but embraces such modified forms thereof as come within the scope of theclaims.

EXAMPLES Example 1 A Two-Step Enzymatic Modification Method to ReduceImmunoreactivity of Milk Proteins

Summary

A two-step enzymatic approach to reduce immunoreactivity of whey proteinisolate and casein has been studied. The method involves partialhydrolysis of proteins with proteases, followed by repolymerization withmicrobial transglutaminase. Whey protein isolate partially hydrolyzedwith chymotrypsin, trypsin, or thermolysin retained about 80%, 30%, and20% of the original immunoreactivity, respectively. Afterrepolymerization the immunoreactivity was about 45%, 35%, and 5% of theoriginal immunoreactivity, respectively. The immunoreactivity ofhydrolyzed and repolymerized casein was negligible compared to nativecasein. The repolymerized products were partially resistant to in vitrodigestion. Peptides released during digestion of repolymerizedthermolysin-whey protein hydrolysate had less than 5% immunoreactivity,whereas those of whey protein control exhibited a sinusoidalimmunoreactivity ranging from 5-20%. Peptides released during digestionof repolymerized thermolysin-casein hydrolysates had noimmunoreactivity. These results indicated that it is possible to producehypoallergenic milk protein products using the two-step enzymaticmodification method involving thermolysin and transglutaminase.

Introduction

Cow's milk allergy is very prevalent among children under the age ofthree. A significant number of infants allergic to cow's milk proteinalso develop allergy to other food proteins (Zeiger et al., 1999; Ahn etal 2003; Burks et al., 1994). Protein allergy in children is mainlyattributed to IgE-mediated hypersensitivity (Exl & Fritsche 2001).Elicitation of allergenic response of a protein could be either due to asequence-specific epitope or conformational epitope. Studies have shownthat partial enzymatic hydrolysis significantly reduced theallergenicity of proteins (Pahud et al., 1985; Businco et al., 1993;Bindels & Boerma, 1994; Oldaeus et al., 1997; Halken et al., 2000;Rosendal & Barkholt, 2000). However, the definition of ‘partial’hydrolysis is quite arbitrary in terms of the peptide length profile. Asa consequence, some partially hydrolyzed protein products have beenshown to cause severe allergic reactions in some children (Rosendal &Barkholt, 2000; Ragno et al., 1993) due to presence of intact linearepitopes in hydrolysates. Furthermore, protein hydrolysates generallytaste bitter (Wróblewska et al., 2004; Matoba & Hata, 1972; Ney, 1971)and lack desirable functional properties, particularly gelation andtexturization, essential for improving sensorial properties ofhypoallergenic food products.

A promising enzymatic approach to reduce the allergenicity of proteinsis enzymatic crosslinking using enzymes such as transglutaminase(Pedersen et al., 2004; Malandain 2005; Buchert et al., 2008; O'Sullivan& FitzGerald, 2012; Li & Damodaran, 2016). Transglutaminase (TGase)catalyzes a crosslinking reaction between glutamine and lysine residuesin proteins. (Han & Damodaran, 1996; DeJong & Kippelman, 2002; Agyare &Damodaran, 2010). This crosslinking reaction could be inter-molecularand intra-molecular. When inter-molecular crosslinking occurs, which isthe predominant route, the reaction produces branched-chain proteinpolymers (Han & Damodaran, 1996). It is likely that this crosslinkingreaction might alter both conformational and linear epitopes and thusrender the modified protein to be less responsive to IgE binding.However, studies have shown that polymerization of milk proteins, viz.,β-casein and β-lactoglobulin using microbial transglutaminase resultedonly in marginal decrease in their immunoreactivity (Stanic et al.,2010; Olivier et al., 2012; Li & Damodaran, 2016). On the other hand,transglutaminase crosslinking of wheat flour caused a 70% reduction inglutenin immune reactivity, whereas that of ω-gliadin actually increasedin non-competitive ELISA (Leszczynska et al 2006; Palosuo et al 2003).In a recent study, Li and Damodaran (2016) reported thatimmunoreactivity of protein components in heterologous crosslinkedprotein polymers was significantly lower than in homologous crosslinkedprotein polymers. However, a significant fraction of conformational andlinear epitopes were still intact and were readily accessible toantibody binding in some heterologous protein conjugates, such ascrosslinked whey protein-casein, soy protein-casein, and soyprotein-whey protein polymers.

The hypothesis of the present study is that a combination of initialpartial hydrolysis of protein using a suitable protease followed byTGase-catalyzed repolymerization of the hydrolysate could producehypo-immune-reactive protein polymers. This two-step enzymatic approachwould completely disrupt both the integrity and accessibility ofallergenic epitopes to IgE in proteins. This is predicted also toeliminate the bitter flavor often associated with protein hydrolysates.To test this hypothesis, we used trypsin, chymotrypsin, and thermolysinto partially hydrolyze whey protein isolate (WPI) and sodium caseinate(CN) under controlled conditions and repolymerized the resultinghydrolysate using TGase to produce branched chain polymers. Theimmunoreactivity of these hydrolysates and polymers were investigatedusing protein specific ELISA. The digestibility of these branched chainpolymers under simulated gastric-duodenal conditions and theimmunoreactivity of the digests were also studied.

Materials and Methods

Materials

Commercial sodium caseinate was from Agroupur Ingredients (Product No.SR:9710; La Crosse, Wis., USA) and whey protein isolate (WPI) was fromDavisco Foods International Inc., (BiPRO, Lot No. JE045-5-420, EdenPrairie, Minn., USA). Thermolysin (Type X, 30-175 units/mg protein),trypsin (from porcine pancreas, type 2, 1600 BAEE units/mg solid; 1800ATEE units/mg solid), α-chymotrypsin (from bovine pancreas, 83.9units/mg solid; 96 units/mg protein), porcine stomach mucosa pepsin (EC3.4.23.1, activity: 2100 units/mg solid, 2600 units/mg protein), andporcine pancreatin (P7545) were from Sigma-Aldrich (St. Louis, Mo.,USA). Microbial TGase (Activa-TI, 99% maltodextrin and 1% TGase; 100units/g of solid) was from Ajinomoto Food Ingredients (Eddyville, Iowa,USA). The enzyme was used without further purification.

AgraQuant® F.A.S.T Casein ELISA test kit was purchased from Romer LabsInc. (Union, Mo., USA). RIDASCREEN® β-lactoglobulin test kit waspurchased from R-Biopharm AG (Darmstadt, Germany).

WPI Hydrolysis and Repolymerization

For digestion with thermolysin, a 10% (w/w) solution of WPI at pH 7.0was treated with thermolysin at enzyme-to-substrate weight ratios of1/400, 1/1500 and 1/2000 and incubated at 37° C. for 5 min. Thehydrolysis was stopped by heating in a boiling water bath for 8 min.

It is known that whey proteins are partly resistant to proteolysis bytrypsin and chymotrypsin. Therefore, to facilitate proteolysis withchymotrypsin and trypsin, first a 1% (w/w) solution of WPI was heatdenatured in a boiling water bath for 30 min, cooled and lyophilized. A5% (w/w) solution of this denatured WPI in water at pH 7.0 was treatedwith trypsin or chymotrypsin at various enzyme-to-substrate ratios andincubation time combinations, i.e., 1:200 for 30 min; 1:100 for 30 min,and 1:100 for 1 h at 37° C. The hydrolysis reaction was stopped byheating in boiling water bath for 8 min and then lyophilized.

Repolymerization of the WPI hydrolysates using TGase was performed asfollows: A 10% thermolysin hydrolysate, and 5% trypsin and chymotrypsinhydrolysates were incubated separately with TGase (100 units/g ofsubstrate) in the presence of 5 mM β-mercaptoethanol for 24 h at 37° C.Heating the mixture in a boiling water bath for 8 min stopped thereaction.

Casein Hydrolysis and Repolymerization

Aliquots of a 5% w/w solution of sodium caseinate in deionized water atpH 7.0 were incubated with thermolysin at an enzyme to substrate weightratio of 1:1500 for 5 min, 10 min, and 15 min at 37° C. and hydrolysiswas terminated by heating in a boiling water bath for 8 min and thenlyophilized. Casein was hydrolyzed with chymotrypsin and trypsin at anenzyme-to-substrate weight ratio of 1:200 under conditions similar tothermolysin hydrolysis. Time-point samples were taken after 5 min, 10min, and 15 min followed by heat inactivation of the enzyme in boilingwater for 8 min and then the samples were lyophilized. TGase-catalyzedrepolymerization of the above hydrolysates was performed as describedfor WPI hydrolysate.

Soy Protein Isolate (SPI) Hydrolysis and Repolymerization

Thermolysin hydrolysis: 1:200 enzyme to SPI weight ratio, 37 C for 30min, hydrolysis terminated by boiling at 100° C. for 8 min.

Trypsin and chymotrypsin hydrolysis: A 5% SPI solution was first heatdenatured in boiling water for 30 min, cooled down to 37° C. and thentreated with trypsin or chymotrypsin at an enzyme to SPI ratio (w/w) of1:100 for 30 min. Hydrolysis was stopped by incubating in boiling waterbath for 8 min.

Transglutaminase reaction: The hydrolysate was treated withtransglutaminase at an enzyme to substrate weight ratio of 100 Units/gsubstrate at 37° C. for 24 h, followed by inactivation of the enzyme inboiling water for 8 min.

In Vitro Digestion of Repolymerized Protein Polymers

In vitro digestion of repolymerized-protein polymers under simulatedgastro-intestinal conditions was performed as described elsewhere(Dupont et al, 2010; Fu, Abbott, & Hatzos, 2002; Li & Damodaran, 2016).Briefly, protein samples were dissolved (2%) in 0.15 M NaCl and the pHwas adjusted to 2.5 with 1N HCl to simulate the gastric fluidconditions. Porcine stomach mucosa pepsin was added at a 1:20enzyme-to-protein weight ratio and the mixtures were incubated at 37° C.for 1 h. To create the intestinal condition, the pH of the gastricdigest was raised to 6.5 using 1N NaOH and bile salt and bile-Tris wereadded so that the final concentrations of these components were 1.85 mMand 26.1 mM, respectively. To this mixture was added porcine pancreatinat a 1:20 enzyme-to-protein ratio and the mixture was incubated at 37°C. Samples withdrawn at various time intervals during the intestinalphase of digestion were placed in a boiling water bath for 10 min toterminate digestion. The immunoreactivity of the digests was analyzedusing protein-specific ELISA kits.

Electrophoresis

Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) ofprotein samples under reducing conditions was carried out as describedpreviously (Agyare & Damodaran, 2010) using a 12.5% acrylamideseparating and a 4.5% acrylamide stacking slab gel in a Mini-PROTEAN 3apparatus (Bio-Rad Laboratories, Hercules, Calif., USA). A mixture ofmolecular weight standards (11-170 kDa) (Sigma-Aldrich Co., St. Louis,Mo., USA) was also run along with the samples.

To better resolve low molecular weight peptides in some cases,tris/tricine polyacrylamide gel electrophoresis was also performedaccording to Schagger & Von Jalow (1987) using a 16.5% acrylamideseparating and a 4% acrylamide stacking slab gel. A mixture of molecularweight standards (6-180 kDa) (NOVEX, Life technologies, CA, USA) wasalso run along with the samples.

ELISA

Immunoreactivity of control and treated protein samples were studiedusing commercially available protein-specific ELISA kits. Theexperiments were performed as described elsewhere (Li & Damodaran,2016). In the case of WPI, which is a mixture of β-lactoglobulin andα-lactalbumin, the immune-reactivity of WPI was determined using aβ-lactoglobulin-specific competitive ELISA kit. In all ELISAexperiments, the intensity of color products released in the titer wellswas measured at 450 nm in an automated Spectra MAX plus ELISA platereader (Molecular Devices Inc., Sunnyvale, Calif., USA). Theseexperiments were done in duplicate and statistical analyses (analysis ofvariance) of the results were performed using Excel.

Results and Discussion

WPI Hydrolysis

β-LG is known to be very resistant to digestive enzymes, especiallytrypsin and chymotrypsin, but its susceptibility improves upon thermaldenaturation (Reddy et al., 1988; O'Loughlin et al., 2012). Therefore, apre-heat treatment (see methods) was employed to improve thesusceptibility of WPI to proteolysis. Hydrolysis of WPI by trypsin,chymotrypsin, and thermolysin under various conditions is shown in FIGS.1A-1C. It should be noted that even after thermal denaturation in aboiling water bath for 30 min, β-LG in WPI was not completely hydrolyzedby trypsin and chymotrypsin even when hydrolyzed at anenzyme-to-substrate ratio of 1:100 for 1 h, whereas α-LA was completelyhydrolyzed to smaller peptides (FIG. 1A, lanes 7 and 10). On the otherhand, thermolysin was very effective in hydrolyzing both β-LG and α-LAin native WPI to about 3-12 kDa peptides even at an enzyme-to-substrateratio of 1:2000 for 5 min (FIG. 1A, lane 2). WPI was completelyhydrolyzed to small peptides at a thermolysin-to-substrate weight ratioof 1:400, as is evident from faint staining of bands in the SDS-PAGEprofile (FIG. 1A, lane 4). Extensive hydrolysis of WPI may releasesignificant amounts of short peptides with no glutamine residue. Suchpeptides would not participate in TGase-mediated repolymerizationreaction. Thus, limited proteolysis that results in release of peptidesin the MW range of 3-10 kDa is desirable to increase the yield ofcrosslinked polymers during TGase-catalyzed repolymerization ofhydrolysates. Accordingly, the following hydrolysis conditions wereselected for the three proteases: An enzyme-to-substrate ratio of 1:1500and 5 min was used for thermolysin and an enzyme-to-substrate ratio of1:100 and 30 min was used for trypsin and chymotrypsin.

Immunoreactivity of WPI Hydrolysates and Their Repolymerized Products

The native WPI and hydrolyzed WPI formed large polymers when treatedwith TGase (FIG. 1B). The polymerized native WPI showed new smearedbands in the molecular weight range of ˜30 to ˜400 kDa (FIG. 1B, lane2). However, some (˜10%) monomeric β-LG and α-LA were present in thepolymerized sample even after 24 h of treatment with TGase. A similarobservation had been made in previous studies (Han & Damodaran, 1996; Li& Damodaran, 2016). In the case of hydrolysates, thermolysin was veryeffective in hydrolyzing β-LG and α-LA (FIG. 1B, lane 3), whereas asmall amount of intact β-LG and α-LA was left unhydrolyzed in trypticand chymotryptic hydrolysates (FIG. 1B, lanes 4 and 5). When thesehydrolysates were treated with TGase, the intensities of residual β-LGand α-LA bands were greatly reduced, indicating that they along withother peptides in the hydrolysates were copolymerized to high molecularweight polymers by TGase (FIG. 1B, lanes 7 and 8); however, it has to benoted that some residual amount of β-LG was still present along withappearance of a β-LG dimer band (FIG. 1B, lanes 7 and 8). The molecularweight of the heterogeneous crosslinked polymers ranged fromapproximately 6 kDa to well over 400 kDa as evident from the continuoussmeared bands in SDS-PAGE. This wide molecular size distribution mightbe the result of limited availability of glutamine and lysine residuesin peptides of the hydrolysates. Whey proteins contain a lowglutamine-to-lysine ratio. For instance, β-LG contains 10 glutamine and15 lysine residues, whereas α-LA contains 5 glutamine and 12 lysineresidues. As a result, depending on their distribution in the primarysequence and the sites of cleavage by the proteases, it is theoreticallypossible that some of the peptides released in the hydrolysates might bedevoid of glutamine residues. It would not be possible for such peptidesto take part in the TGase-catalyzed polymerization reaction. The lowmolecular weight polymers in FIG. 1B, Lanes 6-8 might be suchpolypeptides.

The immunoreactivity of β-LG in WPI and its fragments containingallergenic epitopes in various enzyme treated WPI samples is shown inFIG. 1C. TGase polymerization of native WPI (WPI-TG) decreased itsimmunoreactivity to 78% of that of native WPI control. Since accordingto the SDS-PAGE profile only a small amount (˜10%) of intact β-LG waspresent in the WPI-TG sample (FIG. 1B, lane 2), only a 22% reduction inimmunoreactivity of the WPI-TG polymers suggests that most of theantigenic epitopes of native β-LG were not disrupted during thepolymerization reaction and they were still easily accessible toantibody binding. Among the WPI hydrolysates, the immunoreactivity ofthe chymotryptic hydrolysate (chymotryptic-WPIH) was 83% and that of thetryptic-WPIH was about 29% of the WPI control.

The high immune-reactivity of chymotryptic-WPIH cannot be totally due toresidual β-LG in the sample, because this residual amount was less than10% of the control WPI whereas the immune reactivity of the sample was83% (FIG. 1B, lanes 1 and 5). This is also true of the tryptic-WPIH.Therefore, these greater than expected immunoreactivity of tryptic andchymotryptic hydrolysates might be due to presence of intact linearepitopes in the peptide fragments, especially in chymotryptic-WPIH. Onthe other hand, the thermolysin hydrolysate (thermolysin-WPIH) exhibitedthe lowest (18%) immunoreactivity, suggesting that among the threeproteases thermolysin was more effective in disrupting allergenicepitopes in WPI. Miller et al (1999) reported that the IgE bindingepitopes of β-LG are found in segments 21-40, 41-60, 107-117, and148-162 of the protein. The amino acid sequences of these segments areSLAMAASDISLLDAQSAPLR (SEQ ID NO:1), VYVEELKPTPEGDLEILLQK (SEQ ID NO:2),MENSAEPEQS (SEQ ID NO:3), and RLSFNPTQLEEQCHI (SEQ ID NO:4),respectively. It should be noted that the interior parts of segments21-40, 107-117, and 148-162 do not contain lysine, arginine, tyrosine,tryptophan, and phenylalanine residues and therefore it is more likelythat these IgE binding epitopes might remain intact in a partiallyhydrolyzed tryptic-WPIH and chymotryptic-WPIH hydrolysates. On the otherhand, however, since thermolysin cleaves on the N-side of peptide bondsof hydrophobic residues, the segments 21-40, 41-60, and 148-162, whichcontain several hydrophobic residues, would be disrupted by thermolysinhydrolysis and thus peptides containing these allergenic epitopes wouldnot be present in the thermolysin-WPIH hydrolysate. The lowimmunoreactivity of thermolysin-WPIH compared to tryptic-WPIH andchymotryptic-WPIH hydrolysates (FIG. 1C) substantiates these arguments.

Upon repolymerization using TGase, the immunoreactivity of the TGpolymers of thermolysin WPI hydrolysate (thermolysin-WPIH-TG) decreasedfrom 18% to 6%, and that of the TG polymers of chymotryptic WPIhydrolysate (chymotryptic-WPIH-TG) decreased from 83% to 44%, indicatingthat the immunoreactive epitopes were further disrupted and/or havebecome masked by the crosslinking reaction. In contrast,repolymerization of tryptic hydrolysate (tryptic-WPIH-TG) did notsignificantly change its immunoreactivity, which remained at 29-31%.(FIG. 1C), suggesting that the configuration of the branched-chainpolymers in tryptic-WPIH-TG was different from those of thethermolysin-WPIH-TG and chymotryptic-WPIH-TG polymers and the epitopeswere as easily accessible in the repolymerized sample as in thehydrolysate to antibody binding. Since trypsin cleaves proteins at theC-end of lysine (and arginine) residues, lysine would be at theC-terminal of the peptides in the hydrolysate. As a result, when treatedwith TGase, the crosslinking would occur between the amine group ofC-terminal (exo) lysine residues (or the N-terminal amino group ofpeptides) and the amide group of endo-glutamine residues, resulting inan exo-endo type only crosslinking between peptides. In contrast, in thecases of chymotryptic and thermolysin hydrolysates, which do not cleaveat lysine and glutamine residues, endo-endo type would be majorcrosslinking between endo-lysine and endo-glutamine residues along withsome exo-endo crosslinking between exo N-terminal amine and endoglutamine residues of peptides. These differences in the mode ofcrosslinking might create branched-chain polymer structures in whichaccessibility of allergenic epitopes to IgE binding may vary.Nevertheless, the data in FIG. 1C clearly indicate that initialhydrolysis of WPI with thermolysin, followed by repolymerization of thehydrolysate with TGase drastically reduces the immunoreactivity of theneo-protein polymers.

Immunoreactivity of In Vitro Digested TG-Polymers of WPI Hydrolysate

Since trypsin is site specific for lysine and arginine residues, andchymotrypsin is specific for tryptophan, tyrosine, and phenylalanine,the repolymerized tryptic-WPIH-TG and chymotryptic-WPIH-TG samples wouldnot contain cleavage sites for trypsin and chymotrypsin, respectively,during the duodenal phase of digestion. Therefore, we limited ourstudies only to examining the immunoreactivity of thethermolysin-WPIH-TG polymers.

The extent of hydrolysis as a function of time of native WPI andthermolysin-WPIH-TG polymers under simulated gastric and duodenalconditions is shown in FIGS. 2A-C. The native WPI was rapidly hydrolyzedto small peptides with only a small amount of β-LG left undigested afterthe first 60 min of gastric phase digestion. The digest contained a ˜10kDa polypeptide as the major component (FIG. 2A). Digestion ofpolypeptides continued during the duodenal phase digestion, however this˜10 kDa polypeptide appeared to be resistant to digestion, as evidencedfrom its very slow disappearance during 180 min of duodenal phasedigestion. In contrast, although most of the thermolysin-WPIH-TGpolymers were digested during 60 min of gastric phase digestion, thedigest still contained some high molecular weight polymers, as evidencedfrom a smeared band in the molecular weight range of 5-100 kDa after 60min of gastric digestion (FIG. 2B). During the duodenal phase ofdigestion, these remaining high molecular weight polymers were veryslowly digested down to lower molecular weight polymers. However, asmeared band in the range of 5-10 kDa molecular weight was still presenteven after 180 min of hydrolysis (FIG. 2B). These seeminglyun-digestible peptides might be remnants of branched-chain polymers thatcould not be further digested because of blocked lysine residues and/orinaccessibility of the remaining peptide bonds to proteases andpeptidases of pancreatin due to steric constraints imposed by branchedchains.

The immunoreactivity of peptides released during the time course of invitro digestion is shown in FIG. 2C. While the immunoreactivity of thenative WPI digests exhibited a sinusoidal pattern, i.e., rising andfalling with digestion time, within the range of 5% to 20% reactivity,the immunoreactivity of the thermolysin-WPIH-TG polymer digest wasconstant at ˜5% throughout the 240 min digestion period, indicating thatgastro-duodenal digestion of thermolysin-WPIH-TG polymers did notrelease any IgE reactive peptides. Previously, it has been shown thatwhen WPI-TG polymers (i.e., intact WPI polymerized with TGase) weresubjected to simulated gastro-duodenal digestion, its digest alsoexhibited a sinusoidal immunoreactivity pattern similar to native WPIranging from 5% to 20% as a function of digestion time (Li & Damodaran,2016). The absence of this pattern with the thermolysin-WPIH-TG polymersindicates that all potential linear antigenic epitopes were effectivelyeliminated/disrupted in this two-step enzymatically modified WPI. Theallergenicity of WPI and partially hydrolyzed WPI often observed inpatients might be due to this residual 20% immunoreactivity of thedigested products, and this level of immunoreactivity might besufficient enough to trigger a strong gut immune response. However, itis possible that the low (<5%) immunoreactivity of thermolysin-WPIH-TGpolymers digests is predicted not to elicit a strong response from thegut immune system of patients allergic to milk proteins.

Casein Hydrolysate and its Repolymerized Products

Caseins are highly flexible proteins and, as a result, are readilydigested by proteases. Therefore, optimization of partial hydrolysisconditions to produce peptide fragments in the MW range of 3-10 kDa wasnecessary for the subsequent TGase-catalyzed repolymerization reaction.FIG. 3A shows the SDS-PAGE profile of casein digested with thermolysin,trypsin, and chymotrypsin at various enzyme-to-substrate ratios andhydrolysis times. Among the three thermolysin hydrolysates, thosecorresponding to 1:2000 and 1:1500 enzyme-to-substrate ratios showed nonoticeable difference in the SDS-PAGE profile, while the 1:800 samplewas over hydrolyzed as seen from the reduced intensity of the coomassieblue staining. To choose between 1:2000 and 1:1500 enzyme-to-substrateratios, the immunoreactivity of both these hydrolysates were testedusing casein-specific ELISA. The result showed that both these sampleshad very low immunoreactivity (data not shown). However, the onehydrolyzed at 1:1500 enzyme-to-substrate ratio had lower activity thanthe one at 1:2000 enzyme-to-substrate ratio. Therefore, the 1:1500enzyme-to-substrate ratio was chosen for subsequent steps. Similarly,the 1:400 enzyme-to-substrate ratio/10 min and the 1:200enzyme-to-substrate ratio/10 min hydrolysis conditions were chosen asoptimum conditions for tryptic and chymotryptic digestions,respectively.

The SDS-PAGE profiles of thermolysin, tryptic, and chymotryptichydrolysates of casein (CNH) and their repolymerized polymers (CNH-TG)are shown in FIG. 3B. Under the hydrolysis condition used, the molecularweights of peptides in all the three hydrolysates were in the range ofabout 10 to 20 kDa (FIG. 3B, lanes 3-5). Upon treatment with TGase,casein and its hydrolysates were able to form large MW polymers (FIG.3B, lanes 2, 6-8). Some of these polymers could not pass through thestacking and separating gels. In the cases of repolymerizedhydrolysates, the smeared bands from 10 kDa to top of the separating andstacking gels (FIG. 3B, lanes 6-8) indicated that they contained aheterogeneous mixture of crosslinked polymer with wide ranging molecularweights. As in the case of WPIH-TG polymers (FIG. 1B, lanes 6-8), thiswide molecular size distribution might be the result of limitedavailability of glutamine and lysine residues in peptides of thehydrolysates. Caseins contain approximately equal amount of glutamineand lysine residues. However, depending on their distribution in theprimary structure and the sites of cleavage by the proteases, it islikely that some of the peptides in the hydrolysate might not contain orcontain only a limited number of glutamine residues, which would limittheir participation in the polymerization reaction. The wide molecularsize distribution of CN-TG polymers (FIG. 3B, lanes 6-8) might be areflection of this phenomenon.

Immunoreactivity of Casein Hydrolysates and their TG-Polymers

Polymerization of intact casein (CN) using TGase decreased itsimmunoreactivity to about 70% of the control (FIG. 3C), indicating thata majority of antigenic epitopes (both conformational and linearepitopes) was still accessible to IgE binding in CN-TG polymers. On theother hand, the thermolysin, tryptic, and chymotryptic hydrolysates ofCN showed no immunoreactivity. In addition, the TG-polymers of these CNhydrolysates (CNH-TG) also showed no immunoreactivity, indicating thatalmost all antigenic epitopes in casein were disrupted by hydrolysis;repolymerization of the peptides in the hydrolysate to large MW polymersdid not result in reformation of any conformational epitopes.

FIGS. 4A and 4B show the digestibility of native CN andthermolysin-CNH-TG polymers, respectively, in the two-step simulatedgastric and duodenal phase digestion system. Native CN was readilydigested to 10-15 kDa peptides during the gastric phase digestion andthese peptides disappeared during the duodenal phase digestion. In thecase of thermolysin-CNH-TG polymers, all the high MW polymers that couldnot enter the stacking and separating gels were digested completely to<60 kDa polypeptides during the 60 min gastric phase digestion. Thesepolypeptides were further digested to <15 kDa peptides during the 180min duodenal phase digestion. However, as in the case of WPI, these <15kDa polypeptides appeared to be resistant to further break down todipeptides and amino acids even after 180 min of duodenal phasedigestion, indicating that these were the remnants of branched-chainpolymers that no site-specific enzyme and endo- and exo-peptidases inpancreatin could digest. It is possible that a longer than 180 minincubation time with pancreatin could have further digested these limitpolypeptides. However, since the gastro-intestinal transit time of foodafter intake is typically 3-4 h, it is unlikely that these limitpolypeptides would be digested under normal in vivo conditions.

The immunoreactivity of peptides released during the time course of invitro digestion of thermolysin-CNH-TG polymers is shown in FIG. 4C. Theimmunoreactivity of digested native casein and the thermolysin-CNH-TGpolymers was almost zero throughout the 240 min digestion period,indicating that gastro-duodenal digestion of thermolysin-CNH-TG polymersdid not release any antigenic peptides.

SPI Experiments

The experiments outlined above conducted on WPI and CN were conducted onSPI. The results of the experiments conducted on SPI were similar tothose for the WPI and CN experiments (FIGS. 5-8 ).

Conclusion

Both caseins and whey proteins are known to be strongly allergenic(Baudon, Mougenot, & Didry, 1987; Docena et al., 1996). Caseinhydrolysate has been found to be safe in infants allergic to cow's milk(Sampson, et al., 1991). However, partially hydrolyzed whey protein hasbeen shown to trigger allergic symptoms in children with cow's milkallergy (Ragno et al., 1993). Those findings tentatively suggested thatallergenicity of hydrolyzed milk proteins essentially stemmed frompartially hydrolyzed whey protein components. The results of the currentstudy, which is based on ELISA, agree with results of those earlier invivo studies.

The results of the present study also strongly indicate that theimmunoreactivity of hydrolyzed milk proteins, viz., whey proteins andcasein, can be significantly reduced and/or eliminated using a two-stepenzymatic process, namely initial partial hydrolysis using thermolysin,trypsin, or chymotrypsin, followed by repolymerization of thehydrolysate using TGase. Among the proteases, thermolysin is the mosteffective in disrupting allergenic epitopes in whey proteins. Uponrepolymerization, the immunoreactivity of thermolysin-WPIH-TG polymerswas the lowest (˜5% of the control WPI), whereas the immunoreactivity oftryptic-WPIH-TG and chymotryptic-WPIH-TG polymers were at unacceptablelevels of 35% and 45%, respectively. Likewise, the thermolysin-CN-TGpolymers also did not have any immunoreactivity. In addition, digestionof the repolymerized CN and WPI hydrolysates under simulatedgastro-duodenal conditions did not release IgE reactive peptides duringthe 240 min time course of digestion. This two-step enzymaticmodification method is predicted not only to produce hypoallergenicprotein polymers, but also to help in alleviating undesirable sensoryproperties, e.g., bitter flavor, associated with protein hydrolysates.

Findings for SPI were similar to those found for CN and WPI.

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Example 2 Nanostructure and Functionality of Enzymatically RepolymerizedWhey Protein Hydrolysate

Summary

Whey proteins (WPI) were polymerized with transglutaminase (TGase)before and after partially hydrolyzing the protein with thermolysin toproduce protein nanoparticles/polymers. Electrophoresis and atomic forcemicroscopy (AFM) were used to determine the size and structuralcharacteristics of the polymers. The foaming and emulsifying propertiesof these nanoparticles were studied. The polymerized WPI (WPI-TG)produced more stable foams than the repolymerized WPI hydrolysate(WPIH-TG). In contrast, WPIH-TG produced better emulsions with betterstorage stability than WPI-TG emulsions. These differences were due totheir structure and electrostatic properties: The WPI-TG particles werelinear, less than 100 nm in size with lower net negative charge, whereasthe WPIH-TG polymers were much larger and were highly negatively chargedas judged from zeta potential. This suggested that while proteinnanoparticles may provide Pickering stability to both emulsions andfoams, strong lateral electrostatic repulsion between nanoparticleswithin the adsorbed film destabilizes foams but not emulsions.

Introduction

Dispersed systems, such as foams and emulsions, can be stabilized usingsoluble surfactants and by using hydrophilic nano- and micro-particles.While soluble surfactants, such as proteins and small moleculeamphiphiles, stabilize dispersed systems by adsorbing to the air-wateror oil-water interface and reducing the interfacial tension, nano- andmicro-particles stabilize emulsions and foams through a phenomenon knownas Pickering stabilization (Binks, 2002; Hunter, Pugh, Franks, &Jameson, 2008; Kalashnikova, Bizot, Cathala, & Capron, 2011). Studieshave shown that chitin and cellulose nanocrystals, silica nanoparticles,hydrophobically modified starch particles, and spore particles were ableto impart Pickering stabilization to oil-in-water emulsions (Tzoumaki,Moschakis, Kiosseoglou, & Biliaderis, 2011; Yusoff, & Murray, 2011;Kalashnikova, Bizot, Cathala, & Capron, 2011; Binks et al, 2011; Pichot,Spyropoulos, & Norton, 2009). This stabilizing effect of nanoparticlesis simply related to binding of the particles to the oil droplet surfaceand forming a physical barrier against coalescence of the dispersedphase.

Soluble globular proteins are highly surface-active due to theiramphiphilic nature, but they do not stabilize dispersed systems by thePickering mechanism. Instead, they readily adsorb to fluid-fluidinterfaces, reduce the interfacial tension, form a viscoelastic film atinterfaces, and stabilize emulsions and foams against coalescencethrough a combination of electrostatic and steric repulsive forces(Damodaran, 2005). However, stable protein and protein-polysaccharidenanoparticles fabricated by using different methods (Dickinson, 2010;Turgeon, Smith, & Sanchez, 2007; Santipanichwong, Suphantharika, Weiss,& McClements, 2008) might have the potential to impart Pickeringstability, in addition to their surface activity and film formingability, to foams and emulsions.

Protein nanoparticles are generally produced by thermal aggregation ofproteins under controlled conditions (Lee et al, 2016; Matalanis, Jones,& McClements, 2011; Zhu and Damodaran, 1994). Such aggregates are formedvia noncovalent interactions as well as via sulfhydryl-disulfideinterchange interaction between denatured protein molecules. In thesetypes of nano-aggregates, the charge characteristics of the primaryprotein molecules are not greatly altered as there is no net loss ofamino and carboxyl groups. Protein nanoparticles or nano-structures alsocan be produced via enzymatic crosslinking of native and/or partiallydenatured proteins using enzymes such as transglutaminase (TGase)(Agyare & Damodaran, 2010). Since primary amino groups and glutamineresidues are consumed in this crosslinking reaction, the proteinnanoparticles produced by this method have greater negative chargedensity than the uncrosslinked protein molecule in the neutral pH range.Another appealing approach is to first enzymatically hydrolyze theprotein and then enzymatically repolymerize the hydrolysate using TGaseto produce a branched chain protein polymer/nanoparticle. Althoughpeptide bond hydrolysis produces new α-amino and α-carboxyl groups, thepositive charge on the α-amino group (pKa=7.8) is less than the negativecharge on the α-carboxyl group (pKa=4.6) at pH 7.0. As a result,nanoparticles obtained with repolymerized protein hydrolysate would bemore negatively charged than the nanoparticles obtained with polymerizedintact protein. Even though the protein origin is same, thenanoparticles obtained by these two different routes might possessdifferent functionality.

The major objective of the present study was to investigate theinterfacial properties of enzymatically crosslinked whey proteinnanoparticles. The hypothesis of this study was that polymerizing nativeand partially hydrolyzed whey proteins using TGase would produce highlynegatively charged polydispersed nanoparticles. In addition to reducinginterfacial tension, these nanoparticles could impart Pickeringstabilization to foams and emulsions.

Materials and Methods

Materials

Whey protein isolate (WPI) was obtained from Davisco Foods InternationalInc., (Eden Prairie, Minn., USA). Thermolysin (Type X, 30-175 units/mgprotein) was purchased from Sigma-Aldrich (St. Louis, Mo., USA).Microbial transglutaminase (TGase) used in this study (Activa-TI, 99%maltodextrin and 1% TGase, 100 units/g solid) was from Ajinomoto FoodIngredients (Eddyville, Iowa, USA). The enzyme was used without furtherpurification.

Preparation of Branched-Chain WPI Polymers

To prepare crosslinked native WPI polymers, a 5% (w/w) WPI solution indeionized water containing 5 mM β-mercaptoethanol at pH 7.0 was treatedwith TGase at an enzyme to substrate ratio of 100 units/gram substrate.The polymerization reaction was carried out for 4 h at 37° C. andterminated by heating in boiling water for 8 min. The sample was thendialyzed using 6-8 kDa molecular weight cutoff membrane against water atpH 7.0 for 24 h to remove maltodextrin, followed by centrifugation at7100 g for 10 min to remove any insoluble polymers. The solution wasthen lyophilized and stored at −20° C.

To prepare protein nanoparticles from WPI hydrolysate, first a 5% (w/w)WPI solution in deionized water, adjusted to pH 7.0, was preheated to70° C. in a water bath for 30 min. Thermolysin was then added at anenzyme-to-substrate ratio of 1:6000 (w/w), and hydrolysis was carriedout at 70° C. for 1 min. Hydrolysis was terminated by incubating in aboiling water bath for 8 min. The sample was lyophilized and stored at−20° C. To repolymerize the hydrolysate, a 5% w/w solution of thehydrolysate in water at pH 7.0 containing 5 mM 3-mercaptoethanol wastreated with 100 units of TGase/gram substrate and incubated at 37° C.for 4 h. Subsequent heating in boiling water for 8 min terminated thepolymerization reaction. The solution was then dialyzed using 6-8 kDamolecular weight cutoff membranes against water at pH 7.0 for 24 h toremove maltodextrin, salts, and any low molecular weight peptides. Thedialyzed sample was then centrifuged at 7100 g for 10 min to remove anyinsoluble polymers. The solution was lyophilized and stored at −20° C.Several batches of the polymers were produced under identicalexperimental conditions; these samples showed similar molecular massprofiles in SDS-PAGE electrophoresis.

Determination of Degree of Hydrolysis (DH)

The degree of hydrolysis (DH) of thermolysin-digested WPI was determinedby the pH-Stat method (Adler-Nissen, 1986) using a Mettler Toledo DL50Autotritrator (Mettler Toledo, Greifensee, Switzerland). DH wascalculated using the following equation:DH=[V _(NaOH) ×N _(NaOH))/(α×m×h _(tot))]×100%where α was the degree of dissociation of α-amino groups, m was the massof protein (g), and h_(tot) was the total number of peptide bonds in theprotein (meq/g protein). The concentration of NaOH used was 0.05N. The αvalue depended on temperature and pH, which were maintained at 70° C.and 7.0, respectively. The corresponding α value and h_(tot) for WPIwere 0.6 and 8.8, respectively (Adler-Nissen, 1986). In theseexperiments, the hydrolysis conditions were chosen such that the DH ofthe hydrolysate was only about ˜1%.Electrophoresis

SDS-PAGE of protein samples under reducing and non-reducing conditionswas performed as described previously (Agyare & Damodaran, 2010) using a12.5% acrylamide separating and a 4.5% acrylamide stacking slab gel.

Apparatus for Measuring Foaming Properties

Evaluation of foaming capacity and foam stability was carried out in aLaplace pressure apparatus. The apparatus used for this purpose isdescribed in detail elsewhere (Yu & Damodaran (1991a). The physicalprinciple behind this method is the Laplace pressure: According toLaplace, the pressure inside a foam bubble is greater than the pressureoutside and this difference is given byΔP=2γ/r  (1)where γ is the surface tension and r is the radius of the bubble. On thebasis of this, the equation of state of foam in a closed environment canbe shown to be,3VΔP+2γΔA=0  (2)where ΔP and ΔA are the change in pressure and interfacial area,respectively, and V is the volume of the apparatus. According toequation 2, any change in the interfacial area of the foam, i.e. as aresult of breakage of foam with time, will cause a correspondingincrease in the pressure inside the closed vessel. The total initialinterfacial area (A₀) at time t=0 can be obtained from total change inpressure inside the closed vessel at infinite time when the entire foamhas collapsed. Thus, at t=t_(∞),A ₀=3VΔP _(∞)/2γ  (3)The interfacial area of the foam at any time t during foam decay (A_(t))is given byA _(t)=3V(ΔP _(∞) −P _(t))/2γ.  (4)Since foam decay is assumed to follow first order kinetics, and sincetwo distinct macroscopic processes, viz., liquid drainage anddisproportionation (Oswald ripening), are involved in foam decay, thekinetics of foam decay can be expressed as a biphasic first orderprocess,A _(t) /A ₀ =Q _(g) exp(−k _(g) t)+Q _(d) exp(−k _(d) t),  (5)where k_(g) and k_(d) are first-order rate constants for thegravitational drainage and disproportionation processes, respectively(Yu & Damodaran, 1991a). While A_(o) provides information on the abilityof a protein to create foam, i.e. foamability, the kinetics of foamdecay provides information on foam stability. The rate constants aredetermined from nonlinear curve fitting of the foam decay data toequation 5.

The foaming properties of native WPI and enzyme modified WPI werestudied using the Laplace pressure apparatus exactly as describedelsewhere (Yu & Damodaran, 1991a, b). Briefly, 20 mL of protein solution(5% w/w) in 20 mM phosphate buffer was preequilibrated in a water bathat 25° C. for one hour before being loaded into the fritted glass tubeof the apparatus housed in an environmental incubator maintained at 25°C. Nitrogen gas was bubbled through the protein solution at a rate of 20mL/min until the foam rose to a premarked point at the top of the foamcolumn. Closing all valves then closed the system. An in-built pressuretransducer in the apparatus monitored the time-dependent increase ofpressure inside the foam column. The pressure was then converted tointerfacial area of the foam using equation 4. The surface tension γ ofthe protein solution was determined using the Whilhelmy plate method (Xu& Damodaran, 1992).

Emulsion Preparation and Analysis

Emulsions were prepared with 1% (w/w) protein solution in 20 mMphosphate buffer (pH 7.0) and 20% (v/v) soybean oil for a total volumeof 3.5 mL. Coarse emulsions were prepared by sonication using a BransonSonifier 450 (BRANSON Ultrasonics Corp., CT, USA). The coarse emulsionswere then homogenized in a high-pressure homogenizer (EmulsiFlex-B3,Avestin, Inc., Ottawa, Canada) at an operating hydraulic pressure of 152MPa with three passes. Emulsions were stored at room temperature in thedark and the particle size distribution was determined over the courseof one month.

Emulsion droplet size distributions were measured using a 90Plus/BI-MASparticle sizer (Brookhaven Instruments Corp., NY, USA). Emulsions werediluted 1500-fold using deionized water prior to the measurement. Therate of change of emulsion interfacial area, as calculated fromMultimodal Size Distribution (MSD) charts for diameter-by-volume (d32)data, was used to determine emulsion stability during storage over onemonth. Zeta potential of emulsion droplets in deionized water and in 0.1M NaCl was measured using the same instrument.

Surface Tension

Surface pressure of the protein solution was measured by the Wilhelmyplate method using an LB trough (KSV 2000, KSV Instruments Ltd.,Finland) as described elsewhere (Xu & Damodaran, 1992). In a typicalexperiment, 100 mL of 10⁻⁴% (w/v) protein solution in 10 mM phosphatebuffered saline solution (I=0.1M), pH 7.0, was poured into a Teflontrough. The surface was vacuum aspirated with a clean fine glasscapillary to create a clean new aqueous surface. The surface pressuredevelopment was recorded over a 24 h period without stirring the bulkphase. Preliminary experiments indicated that a 10⁻⁴% (w/v) bulkconcentration of WPI was sufficient to form a saturated monolayer at theair-water interface at equilibrium.

pH-Turbidity Measurement

The pH versus apparent solubility profiles of native and enzyme modifiedWPI samples were determined by measuring the turbidity of 0.1% proteindispersion in the pH range 2 to 10 (Liu, Elmer, Low, & Nickerson, 2010;Nath, Patrickios, & Hatton, 1995). The turbidity of the solutions wasmeasured as absorbance at 500 nm using a UV-visible spectrophotometer(Shimadzu UV-P1601 PC, Shimadzu Corp., Kyoto, Japan).

Atomic Force Microscopy

Topographical images of native and polymerized WPI samples were obtainedusing a BioScope Catalyst atomic force microscope (Bruker Corporation,Santa Barbara, Calif.) operated in peak force tapping (PFT) mode.Protein solutions were diluted to 10 ppb in water at pH 7.0. Two μL ofthe solution was drop-deposited onto a freshly cleaved mica surface thathad been fixed with 0.01% w/v poly-L-lysine solution and washed toremove any salts. The slides were air dried until no liquid was visibleon the mica. The topographical image data were analyzed using NanoScopeAnalysis software (version 1.40, Bruker Corporation, Santa Barbara,Calif.).

Statistical Analysis

Analytical replicates were performed at least two times to report meansand standard deviations where appropriate. Statistical analysis wasconducted using JMP Statistical Discovery™ from SAS. P-values less than0.05 were considered statistically significant.

Results and Discussion

The rationale for selecting thermolysin as opposed to other proteasesfor making WPI hydrolysate (WPIH) was that this enzyme hydrolyzespeptide bonds at the N-side of hydrophobic amino acid residues. Thismode of cleavage is expected to disrupt the hydrophobicsequences/segments in the protein as well as release peptides withlysine and glutamine residues mostly in the inner parts of releasedpeptides. The degree of hydrolysis (DH) was intentionally limited to˜1%, as extensive digestion of WPI would have produced considerableamount of short peptides with no Lys and/or Gln residues available forthe TGase-catalyzed repolymerization reaction.

SDS-PAGE Analysis of Crosslinked Proteins

The SDS-PAGE profiles of untreated WPI, WPIH, TGase-treated WPI(WPI-TG), and TGase-treated WPIH (WPIH-TG) under reducing andnon-reducing conditions are shown in FIGS. 9A and 9B. Bands of β-LG withmolecular weight (MW) of 18.3 kDa and α-LA with MW of 14.4 kDa werevisible in the control WPI (FIG. 9A, lane 2). The WPI-TG samplecontained high MW polymers that were unable to penetrate the stackingand separating gels under reducing conditions (FIG. 9A, lane 3). It hasbeen previously shown that α-LA was a better substrate for TGase thanβ-LG (Damodaran & Agyare, 2013), and therefore it is reasonable that aconsiderable amount of β-LG remained in the monomeric state after 4 h ofpolymerization (FIG. 9A, lane 3). The WPIH sample produced a smearedband with polypeptides below the size of β-LG (FIG. 9A, lane 4). Asshown in FIG. 9A, lane 5, the WPIH-TG sample contained high MW polymersthat were unable to penetrate the stacking and separating gels inaddition to a broad size distribution of polymers in the separating gel.Since enzyme-treated WPI samples were subsequently heat treated toinactivate the enzymes, it is very likely that some of the polymers inthese samples might be S-S crosslinked polymers in addition to TGasecrosslinked polymers (Zhu & Damodaran, 1994). To assess thispossibility, SDS-PAGE of these samples was run under non-reducingconditions and the results are shown in FIG. 9B. A comparison of lanes 3in FIGS. 9A and 9B indicates that a majority of polymers in the WPI-TGsample were TGase crosslinked polymers. Comparison of lanes 4 and 5 inFIGS. 9A and 9B suggest that S-S crosslinked polymers were also presentin the WPIH and WPIH-TG samples, as revealed from increased intensity ofbands in the >20 kDa region in the non-reducing SDS-PAGE gel.Nevertheless, the amount of TGase crosslinked polymers that could notpass through the stacking and separating gels was high in both WPI-TGand WPIH-TG samples. Furthermore, since functionality tests on thesesamples were done under non-reducing conditions, the MW profiles shownin FIG. 9B, lanes 3-5 better represent the actual size distribution ofthese crosslinked protein polymers.

Atomic Force Microscopy

The topographical images of native and crosslinked WPI are shown inFIGS. 10A-10C2. Native WPI existed as tiny spherical particles (FIG.10A), which were about 2-3 nm in diameter expected for β-LG and α-LA atpH 7.0. Few large aggregates were also seen, but those might bedisulfide crosslinked and/or hydrophobically aggregated particles formedduring isolation and spray drying of commercial WPI.

The WPI-TG sample contained a heterogeneous mixture of mostly linearstrands of crosslinked WPI with about 4 nm in height and less than 100nm in length (FIGS. 10B1 and 10B2). The overall shape of these particlesin solution cannot be surmised from AFM images, as it is possible thatprotein nanoparticles may deform or flatten when dried for AFM (Saricay,Dhayal, Wierenga, & de Vries, 2012). A close-up view revealed distinctlinear polymers both in individual and in aggregated states. On theother hand, the WPIH-TG particles were much larger than the WPI-TGparticles, and they contained both spherical clusters as well as linearpolymers with about 10 nm in height/diameter and the length ranging from50 nm to more than 100 nm (FIGS. 10C1 and 10C2).

pH-Turbidity

The native WPI showed excellent solubility in the pH range 2.0-10.0(FIG. 11 ). In contrast, both WPI-TG and WPIH-TG polymers exhibitedtypical pH-turbidity profiles with minimum solubility (or maximumturbidity) at about pH 5.0 to 5.3. This loss of solubility near theisoelectric point of whey proteins was likely the result of denaturationduring the heating step to inactivate the protease. However, it has beenpreviously reported that even in the absence of the heating step,incubation of β-LG with TGase caused alterations in thehydrophobic-to-hydrophilic balance of the protein surface due tocrosslinking per se, which caused precipitation of β-LG at around pH 4.0to 5.0 (Damodaran & Agyare, 2013). The WPIH-TG solution remained as atranslucent colloidal solution at pH>7.0 even after centrifugation at5000 g for 10 min (FIG. 12 ), which indicated that the large molecularweight WPIH-TG polymers were truly in a stable colloidal state. TheWPI-TG solutions were also translucent, but more transparent thanWPIH-TG in the pH range 3.0>pH>7.0. The slight turbidity seen in theWPI-TG solution at pH 7.0 might be due to ˜100 nm size crosslinkedpolymers. The difference in the appearances of WPI-TG and WPIH-TGsolutions essentially reflects differences in the size distribution ofthe crosslinked polymers in these samples (see FIGS. 10B1, 10B2, 10C1,and 10C2).

Foaming Properties

Preliminary experiments indicated that sufficient foam to fill the foamcolumn (92 mL) of the Laplace pressure apparatus was not possible with a1% (w/w) solution of native WPI. Thus, a 5% (w/w) protein concentrationwas used in all experiments. The kinetics of surface area decay ofnative WPI, WPI-TG, WPIH and WPIH-TG foams are presented in FIG. 13A.The decay of these foams generally followed nonlinear first orderkinetics, which suggested apparent involvement of at least two kineticphases as described by equation 5. These two processes representgravitational drainage of liquid from the lamella and disproportionationof gas bubbles due to inter-bubble gas diffusion, which are fundamentalprocesses in foam decay (Yu & Damodaran, 1991a). Therefore, regardlessof biphasic or monophasic first order kinetics, it is reasonable toassume that both events occur during foam decay. Since inter-bubble gasdiffusion would be significant only below a critical film thickness, thefirst kinetic phase can be attributed mostly to gravitational drainage(Yu & Damodaran, 1991a, b). The rate constants of drainage anddisproportionation were calculated as described by Yu and Damodaran(1991, a, b). These values are given in Table 1.

TABLE 1 Foaming properties of native and various enzyme-modified WPIsamples. Foaming Equilibrium surface Sample k_(g) (min⁻¹) k_(d) (min⁻¹)time(s) A₀ × 10⁻³ (cm²) pressure (mN/m)¹ NativeWPI 0.0075 ± 0.0007^(B)0.0064 ± 0.0010^(B) 44.7 ± 5.0^(A) 19.7 ± 5.3^(A) 18.8 ± 0.3371^(A)WPI-TG 0.0045 ± 0^(B) 0.0116 ± 0.0068^(A)   32 ± 0^(B) 19.5 ± 0.06^(A)23.5 ± 0.3536^(B) WPI-H  0.009 ± 0.0011^(A) 0.0249 ± 0.0025^(A) 28.3 ±4.7^(B) 17.4 ± 0.4^(A) 16.4 ± 0.5132^(C) WPI-H-TG 0.0101 ± 0.0014^(A)0.0187 ± 0.0047^(A) 25.0 ± 3.0^(B) 18.1 ± 2.2^(A) 14.6 ± 0.7095^(D)^(A-D)Different letters denote statistical difference within eachcolumn. ¹The equilibrium surface pressure of a 10⁻⁴% solution after 24h. k_(g) and k_(d) are gravitational drainage and disproportionationrate constants, respectively. A₀ is the total initial surface area ofthe foam.

Native WPI followed a monophasic first order kinetics, suggesting thatthe macroscopic events of liquid drainage and disproportionation werehappening simultaneously and the rate constants of each were equal inmagnitude. In contrast, the foam of WPI-TG, which had crosslinkedpolymer particles in the size range of <100 nm (FIGS. 10B1 and 10B2),exhibited a convex-type biphasic first order decay. The WPI-TG foam wasmore stable than the native WPI foam for a period of 100 min and thencollapsed thereafter, indicating that liquid drainage was therate-limiting step in this foam. The gravitational drainage rateconstant k_(g) of WPI foam was almost twice that of WPI-TG foam (Table1), indicating that the large linear polymer particles in WPI-TG (FIGS.10B1 and 10B2) were responsible for retarding the gravitational drainagerate. The transformation from a linear (native WPI) to convex-type firstorder decay behavior (WPI-TG) reflects that the crosslinked proteinnanoparticles impart a fundamental change to physical properties of theWPI-TG interfacial film. This might be related to the Pickering effectof large polymers/nanoparticles in addition to their inherent surfaceactivity.

In contrast, in the case of WPIH and WPIH-TG foams while they alsoexhibited convex-type biphasic first order decay, they collapsed rapidlyfrom the start (FIG. 13A). It should be noted that while the particlesize of crosslinked polymers in WPI-TG was <100 nm, it was >100 nm inWPIH-TG polymers (FIGS. 10B1, 10B2, 10C1, and 10C2). Therefore, onewould expect a greater Pickering effect in WPIH-TG-stabilized foam. Oneof the possible reasons for this dichotomy could be that, as discussedbelow (Emulsion stability section), the WPIH and WPIH-TG particles aremore highly negatively charged than the WPI-TG polymers owing to newlycreated (as a result of partial hydrolysis of WPI) C-terminal carboxylgroups of the peptide fragments in these polymers. As a result, stronglateral electrostatic repulsive interactions between adsorbed WPIH-TG(and WPIH) particles within the interfacial film mightrupture/destabilize the foam film, resulting in a faster rate ofcollapse. This charge-related destabilizing effect might be far moredetrimental than any Pickering stabilization imparted by theseparticles. Thus, it appears that it is not just the size, but also theelectrostatic properties of the particles also play a role inPickering-stabilized foams.

The foaming time and initial interfacial area (A₀) of foams arepresented in Table 1. Foamability is defined here as the initial totalsurface area A₀ of the foam, as calculated from ΔP_(∞) using equation 3.In general, longer foaming time corresponded with larger interfacialarea. Bubbling of native WPI solution produced the finest and mostuniform distribution of bubbles, giving the appearance of denser foamwith larger A₀. On the other hand, WPI-TG, WPIH, and WPIH-TG foamsvisually appeared to be polydispersed bubbles of varying sizes. Thelarge bubbles visually observed in the WPIH and WPIH-TG foams alsoappeared more polyhedral in shape than the native WPI and WPI-TG foams.Even though native WPI and WPI-TG appeared to have produced higherinitial interfacial areas, no statistically significant difference in A₀was found between any of the samples despite qualitative differences(Table 1). Compared to native WPI, foaming times were shorter forWPI-TG, WPIH, and WPIH-TG samples. It should be noted that even thoughthe stability of WPI-TG foam was better than native WPI (FIG. 13A), thefoamability (i.e. A₀ value) of WPI was about the same as that of WPI-TG(Table 1). This suggests that the molecular properties that govern thesetwo aspects of foam are quite different: While foamability does notgreatly depend on the molecular size, high molecular weight polymersseem to possess the molecular characteristics needed for foam stability.However, among high molecular weight polymers, highly negatively chargedpolymers, e.g., WPIH and WPIH-TG polymers (see Emulsion stabilitysection), appear to destabilize foams (FIG. 13A).

Highly surface-active proteins produce smaller mean bubble size and thuslarge A₀ (Yu & Damodaran, 1991a, b; Zhu and Damodaran, 1994). Thesurface activities of native and enzyme-modified WPI were determined bystudying the kinetics of adsorption at the air-water interface. FIG. 13Bshows time-dependent increase of surface pressure at the air-waterinterface during adsorption of these proteins from a quiescent bulksolution containing 1.5 μg/mL protein concentration. The relative ratesof surface pressure development as well as the final surface pressureafter 24 h of adsorption followed the order WPI-TG>nativeWPI>WPIH>WPIH-TG. Surface pressure development was fastest for WPI-TGeven though the size of polymers in this sample was larger than thenative WPI (FIG. 13B), which should have decreased its rate ofdiffusion. This suggests that properties other than molecular mass,potentially its conformational rearrangement at the interface, mightcontribute its high surface activity. The relative order of surfaceactivity of native WPI and enzyme-modified WPI samples correlated wellwith relative rates of foam decay, especially liquid drainage rates ofthese foams (Table 1).

The differences among the foaming properties of the treated WPI samplesare inherently related to differences in their structural complexities,molecular/particle surface characteristics, and film-forming ability atthe air/water interface (Damodaran, 2005). For instance, the betterinterfacial adsorption and foaming properties of WPI-TG might be relatedto its mostly linear crosslinked polymer structure observed in the AFMimage (FIGS. 10B1 and 10B2). Such a structure might allow it to moreeffectively adsorb and reduce the interfacial tension than native WPIand WPIH-TG. On the other hand, the highly crosslinked state, the largeparticle size (FIGS. 10C1 and 10C2), and high negative charge of WPIH-TGparticles (see Emulsion stability section) may restrict its adsorptionand film-forming ability at the air-water interface.

Emulsion Stability

Native WPI produced the most stable emulsion with the highestinterfacial area (FIG. 14 ). In contrast, WPI-TG exhibited pooremulsifying ability as judged from much lower emulsion interfacial area.It seems that native WPI most efficiently adsorbed to the oil-waterinterface and created the smallest droplet size distribution, whereasWPI-TG created the largest droplet size distribution, and the WPIH andWPIH-TG samples were intermediate with no significant difference betweenthem. All these emulsions displayed bimodal and trimodal droplet sizedistributions immediately after formation as well as after 27 days ofstorage at room temperature (FIGS. 15A-15H). The larger droplet sizedistribution and lower interfacial area of emulsions made usingenzyme-modified WPI might be due to their large polymer size, whichmight reduce the effective concentration of protein available foradsorbing to or coating of oil droplets during homogenization. In otherwords, unlike in native WPI-stabilized emulsion, only a small percentageof the protein mass of polymerized WPI might be physically at theoil-water interface and the rest might be suspended into the aqueousphase due their large size.

Visual appearances of these emulsions were different: Native WPI andWPIH emulsions appeared smooth and did not stick to the sides of thestorage vial. Both WPI-TG and WPIH-TG emulsions appeared to haveundergone aggregation/flocculation during high-pressure homogenization.With the exception of WPI-TG emulsion, regardless of their initialinterfacial area, all other emulsions were essentially stable over aperiod of 27 days (FIG. 14 ). The interfacial area of the WPI-TGemulsion however decreased from 16000 cm²/mL on day one to about 6200cm²/mL on day 27, which represented a 60% reduction of interfacial area.It is likely that the large colloidal-sized WPIH-TG polymers mightimpart Pickering stabilization of the emulsion. However, it is not clearwhy this Pickering stabilization was not very effective in the case ofWPI-TG emulsions. It is likely that the magnitude of the Pickeringeffect might not be great enough to overcome potentially weak mechanicaland electrostatic properties of the WPI-TG film.

Since the TGase-catalyzed crosslinking reaction consumes positivelycharged lysine residues and other primary amine groups, the TGasetreated WPI samples would be more negatively charged than native WPI atpH 7.0. However, as shown in Table 2, the zeta potential of WPIstabilized emulsion was more negative than the WPI-TG stabilizedemulsion. This suggests that the amount of WPI-TG adsorbed per unit areaof the emulsion droplet was lesser than the amount of WPI adsorbed onthe emulsion droplet. On the other hand, the zeta potential of emulsionsstabilized by WPIH and WPIH-TG was more negative than the native WPI andWPI-TG stabilized emulsions in deionized water at pH 7.0 (Table 2), butthe difference was very low in 0.1 M NaCl solution. This is quitereasonable because even though hydrolysis of a peptide bond releases oneα-carboxyl and one α-amine group, the net charge on the α-amine group(pKa=7.8) at pH 7.0 would be less than the net charge on the carboxylgroup (pKa=4.6). Furthermore, some of the newly released α-amino groupsmight have participated in the crosslinking reaction and therefore theoverall charge of WPIH (which is in the S-S crosslinked state) andWPIH-TG polymers would be much higher than the native WPI and WPI-TGsamples. After 27 days of storage, the negative zeta potential of allsamples increased slightly with the exception of native WPI, whichdecreased (Table 2). This might be due to some compositional changes,i.e. the ratio of low molecular weight and high molecular wrightpolymers, in the interfacial film with time.

TABLE 2 Zeta Potential of emulsion droplets made with native WPI andenzyme-modified WPI samples at day 1 and after storage for 27 days atroom temperature. Zeta potential (mV) in Zeta potential (mV) inDeionized Deionized water pH 7 water, pH 7, I = 0.1M Sample Day 1 Day 27Day 1 Day 27 Native WPI −34.01 ± 3.94^(A) −27.48 ± 7.85^(A) −26.76 ±3.03^(A) −23.89 ± 7.89^(A) WPI-TG −32.98 ± 1.08^(A)  −36.7 ± 9.52^(A)−19.92 ± 1.72^(B) −25.72 ± 1.23^(A) WPIH  49.96 ± 6.74^(B) −59.86 ±3.51^(C) −28.19 ± 1.94^(A) −30.45 ± 1.73^(B) WPIH-TG  −58.4 ± 5.18^(BC)−62.26 ± 3.08^(C) −30.44 ± 2.21^(B) −31.65 ± 1.44^(B) ^(A-C)Differentletters denote statistical difference within each column.

After two-months of storage, the WPI and WPI-TG emulsions, which hadmuch lower zeta potential than WPIH and WPIH-TG emulsions (Table 2),became a gel, indicating that protein-protein interactions betweenadsorbed protein films of emulsion particles in these emulsions createdan extended network structure over a period of time. This inter-particleinteraction might also involve sulfhydryl-disulfide interchange reactionbetween protein films of emulsion particles (Damodaran & Anand, 1997).In contrast, the WPIH and WPIH-TG emulsions, which had high zetapotential, remained fluid, indicating that the large highly negativelycharged WPIH and WPIH-TG polymers/particles imparted strongelectrostatic and steric repulsion (possibly via the Pickeringmechanism) between emulsion droplets over long period of time andprevented formation of any three dimensional network structure betweenthe droplets.

Conclusions

In the present study, nanoparticles of WPI were prepared by enzymatic(TGase) crosslinking of native protein, and also by repolymerizingpartially hydrolyzed WPI using TGase. As judged from AFM images, theshape of WPI-TG particles was mostly linear and less than 100 nm inlength, whereas WPIH-TG particles were mostly spherical and greater than100 nm in size. The results of foaming and emulsification studies showedthat while highly branched and highly negatively charged WPIH-TGpolymers possessed reasonably good emulsifying properties, their foamingproperties were poor. On the other hand, the WPI-TG polymers withcomparatively lower negative charge density possessed excellent foamingproperties, but poor emulsifying properties compared to native WPI andWPIH-TG. These results suggested that while protein nanoparticles impartPickering stabilization to foam, high zeta potential of the particlesdestabilize foams. On the other hand, both high zeta potential andPickering effect of highly branched polymers promote emulsion stability.The results demonstrated that highly stable and non-gelling emulsionscould be made with WPIH-TG polymers; on the other hand, the foamingproperties of WPI could be improved by polymerizing native WPI usingTGase. Since TGase treated WPI hydrolysate exhibits no immunoreactivity(Damodaran and Li, 2017), emulsions and foams produced using WPIH-TG arepredicted to be hypoallergenic.

References

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EXEMPLARY EMBODIMENTS OF THE INVENTION

Embodiment 1. A method of processing protein comprising: hydrolyzing theprotein with a proteolytic agent to generate hydrolyzed peptides; and,optionally, crosslinking the hydrolyzed peptides with a transglutaminaseto generate crosslinked peptides.

Embodiment 2. The method of embodiment 1, comprising the crosslinking.

Embodiment 3. The method of any one of embodiments 1-2, wherein theproteolytic agent comprises a thermolysin.

Embodiment 4. The method of any one of embodiments 1-3, wherein thehydrolyzing comprises partially hydrolyzing the protein and wherein thehydrolyzed peptides are partially hydrolyzed peptides.

Embodiment 5. The method of embodiment 4, wherein the partiallyhydrolyzing comprises hydrolyzing the protein to a degree of hydrolysisof from about 0.1% to about 10%.

Embodiment 6. The method of any one of embodiments 4-5, wherein at leastabout 30% of total mass of the partially hydrolyzed peptides comprisespeptides having a size of from about 3-10 kDa.

Embodiment 7. The method of any one of embodiments 1-6, wherein theprotein comprises an allergenic protein.

Embodiment 8. The method of any one of embodiments 1-7, wherein theprotein comprises at least one of milk protein, soy protein, peanutprotein, and grain protein.

Embodiment 9. The method of any one of embodiments 1-8, wherein theprotein comprises at least one of whey protein isolate and casein.

Embodiment 10. The method of any one of embodiments 1-9, wherein theprotein comprises at least one of β-lactoglobulin and β-casein.

Embodiment 11. The method of any one of embodiments 1-10, wherein theprotein comprises at least one of soy protein isolate and soy proteinconcentrate.

Embodiment 12. The method of any one of embodiments 1-11, wherein theprotein comprises gluten.

Embodiment 13. The method of any one of embodiments 1-12, wherein theprotein comprises an allergenic protein, and wherein the hydrolyzing isperformed under conditions effective for the hydrolyzed peptides to havereduced allergenicity with respect to the protein.

Embodiment 14. The method of any one of embodiments 1-13, wherein theprotein comprises an allergenic protein, and wherein the crosslinking isperformed under conditions effective for the crosslinked peptides tohave reduced allergenicity with respect to the hydrolyzed peptides.

Embodiment 15. The method of any one of embodiments 1-14, wherein theprotein comprises an allergenic protein, and wherein the hydrolyzing andthe crosslinking are performed under conditions effective for thecrosslinked peptides to have reduced allergenicity with respect to theprotein.

Embodiment 16. The method of any one of embodiments 13-15, wherein thereduced allergenicity comprises reduced IgE immunoreactivity.

Embodiment 17. The method of any one of embodiments 1-16, wherein theprotein comprises whey protein, and wherein the hydrolyzing is performedunder conditions effective for the hydrolyzed peptides to have IgEimmunoreactivity less than 25% of IgE immunoreactivity of the protein.

Embodiment 18. The method of any one of embodiments 1-17, wherein theprotein comprises whey protein, and wherein the crosslinking isperformed under conditions effective for the crosslinked peptides tohave IgE immunoreactivity less than 50% of IgE immunoreactivity of thehydrolyzed peptides.

Embodiment 19. The method of any one of embodiments 1-18, wherein theprotein comprises whey protein, and wherein the hydrolyzing and thecrosslinking are performed under conditions effective for thecrosslinked peptides to have IgE immunoreactivity less than 10% of IgEimmunoreactivity of the protein.

Embodiment 20. The method of any one of embodiments 1-19, furthercomprising generating an emulsion with the hydrolyzed peptides and/orthe crosslinked peptides.

Embodiment 21. A product made by the method of any one of embodiments1-20.

Embodiment 22. The product of embodiment 21, wherein the productcomprises an emulsion.

Embodiment 23. The product of embodiment 21, wherein the productcomprises a foam.

Embodiment 24. The product of any one of embodiments 21-23, wherein theproduct comprises a food product.

What is claimed is:
 1. A method of processing a composition comprisingprotein, the method comprising: hydrolyzing at least some of the proteinin the composition with a thermolysin to generate a hydrolysatecomprising hydrolyzed peptides with a size of 3-10 kDa, wherein theprotein in the composition comprises β-lactoglobulin; and crosslinkingat least some of the hydrolyzed peptides in the hydrolysate with atransglutaminase to generate a crosslinked peptide compositioncomprising crosslinked peptides.
 2. The method of claim 1, wherein thehydrolysate has a degree of hydrolysis of from 0.1% to 10%.
 3. Themethod of claim 1, wherein at least 30% of total mass of peptides in thehydrolysate consists of peptides having a size of 3-10 kDa.
 4. Themethod of claim 1, wherein the protein in the composition furthercomprises β-lactalbumin.
 5. The method of claim 1, wherein thecrosslinked peptide composition has reduced β-lactoglobulin-specific IgEimmunoreactivity with respect to the composition.
 6. The method of claim1, wherein the crosslinked peptide composition has reducedβ-lactoglobulin-specific IgE immunoreactivity with respect to thehydrolysate.
 7. The method of claim 1, wherein the hydrolysate hasβ-lactoglobulin-specific IgE immunoreactivity less than 25% ofβ-lactoglobulin-specific IgE immunoreactivity of the composition.
 8. Themethod of claim 1, wherein the crosslinked peptide composition hasβ-lactoglobulin-specific IgE immunoreactivity less than 50% ofβ-lactoglobulin-specific IgE immunoreactivity of the hydrolysate.
 9. Themethod of claim 1, wherein the crosslinked peptide composition hasβ-lactoglobulin-specific IgE immunoreactivity less than 10% ofβ-lactoglobulin-specific IgE immunoreactivity of the composition. 10.The method of claim 9, wherein: the hydrolysate hasβ-lactoglobulin-specific IgE immunoreactivity less than 25% ofβ-lactoglobulin-specific IgE immunoreactivity of the composition; andthe crosslinked peptide composition has β-lactoglobulin-specific IgEimmunoreactivity less than 50% of β-lactoglobulin-specific IgEimmunoreactivity of the hydrolysate.
 11. The method of claim 1, wherein:the crosslinked peptide composition has reduced β-lactoglobulin-specificIgE immunoreactivity with respect to the hydrolysate; and thecrosslinked peptide composition has β-lactoglobulin-specific IgEimmunoreactivity less than 10% of β-lactoglobulin-specific IgEimmunoreactivity of the composition.
 12. The method of claim 11, whereinthe composition is a composition isolated from whey.
 13. A method ofprocessing a composition comprising protein, the method comprising:hydrolyzing at least some of the protein in the composition with athermolysin to generate a hydrolysate, wherein the protein in thecomposition comprises β-lactoglobulin; and crosslinking at least some ofthe hydrolyzed peptides in the hydrolysate with a transglutaminase togenerate a crosslinked peptide composition comprising crosslinkedpeptides.
 14. The method of claim 13, wherein: the crosslinked peptidecomposition has reduced β-lactoglobulin-specific IgE immunoreactivitywith respect to the composition; and the crosslinked peptide compositionhas reduced β-lactoglobulin-specific IgE immunoreactivity with respectto the hydrolysate.
 15. The method of claim 14, wherein the protein inthe composition further comprises β-lactalbumin.
 16. The method of claim15, wherein: the crosslinked peptide composition hasβ-lactoglobulin-specific IgE immunoreactivity less than 10% ofβ-lactoglobulin-specific IgE immunoreactivity of the composition; and atleast 30% of total mass of peptides in the hydrolysate consists ofpeptides having a size of 3-10 kDa.
 17. The method of claim 16, whereinthe hydrolysate has a degree of hydrolysis of from 0.1% to 10%.
 18. Themethod of claim 15, wherein the composition is a composition isolatedfrom whey.
 19. The method of claim 18, wherein: the crosslinked peptidecomposition has β-lactoglobulin-specific IgE immunoreactivity less than10% of β-lactoglobulin-specific IgE immunoreactivity of the composition;and at least 30% of total mass of peptides in the hydrolysate consistsof peptides having a size of 3-10 kDa.
 20. The method of claim 19,wherein the hydrolysate has a degree of hydrolysis of from 0.1% to 10%.